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NUMERICAL INVESTIGATION ON SATURATED BOILING HEAT TRANSFER IN A VERTICAL RECTANGULAR MINICHANNEL

机译:垂直矩形微通道中饱和沸腾传热的数值研究

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A numerical method based on the Euler- Euler model was developed to investigate the mechanism of saturated boiling heat transfer mechanism on upward flow in a vertical rectangular minichannel. This method validated by the experimental data from literature. At the same time, the mechanism of saturated boiling heat transfer was also investigated by ANSYS CFX for Freon R21 at high vapor quality in a vertical rectangular minichannel based on the above numerical method. The results show that the simulation results are good agreement with experimental data from reference and the deviation is within ±15%.The main boiling mechanism is forced convective boiling while the contribution of nucleate boiling is slight for saturated boiling heat transfer at high vapor quality. The evaporation of dispersed liquid phase should be also a main boiling heat transfer mechanism. These results will provide some constructive instructions for the understanding of saturated boiling heat transfer phenomenon in a vertical rectangular minichannel of PFHE.
机译:开发了一种基于Euler-Euler模型的数值方法,以研究饱和沸腾传热机制在垂直矩形小通道中向上流动的机理。该方法得到了来自文献的实验数据的验证。同时,ANSYS CFX还基于上述数值方法,对垂直矩形小通道中氟气较高的氟利昂R21进行了饱和沸腾传热机理的研究。结果表明,模拟结果与参考实验数据吻合良好,偏差在±15%以内。主要的沸腾机理是强制对流沸腾,而在高蒸气质量下,饱和沸腾传热对核沸腾的贡献很小。分散液相的蒸发也应该是主要的沸腾传热机理。这些结果将为理解PFHE的垂直矩形小通道中的饱和沸腾传热现象提供一些建设性的指导。

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